Investigation of the steam reforming of a series of model compounds derived from bio-oil for hydrogen production

2009 ◽  
Vol 88 (3-4) ◽  
pp. 376-385 ◽  
Author(s):  
Xun Hu ◽  
Gongxuan Lu
2010 ◽  
Vol 1279 ◽  
Author(s):  
P. Lan ◽  
Q. L. Xu ◽  
L. H. Lan ◽  
Y. J. Yan ◽  
J. A. Wang

AbstractA Ni/MgO-La2O3-Al2O3 catalyst with Ni as active component, Al2O3 as support, MgO and La2O3 as additives was prepared and its catalytic activity was evaluated in the process of hydrogen production from catalytic steam reforming of bio-oil. In the catalytic evaluation, some typical components present in bio-oil such as acetic acid, butanol, furfural, cyclopentanone and m-cresol were mixed following a certain proportion as model compounds. Reaction parameters like temperature, steam to carbon molar ratio and liquid hourly space velocity were studied with hydrogen yield as index. The optimal reaction conditions were obtained as follows: temperature 750-850 °C, steam to carbon molar ratio 5-9, liquid hourly space velocity 1.5-2.5 h-1. The maximum hydrogen yield was 88.14%. The carbon deposits were formed on the catalyst surface but its content decreased as reaction temperature increased in the bio-oil steam reforming process.


2013 ◽  
Vol 33 (3) ◽  
pp. 1008-1016 ◽  
Author(s):  
Huaqing Xie ◽  
Qingbo Yu ◽  
Kun Wang ◽  
Xiaobo Shi ◽  
Xinhui Li

2015 ◽  
Vol 24 (3) ◽  
pp. 299-308 ◽  
Author(s):  
Huaqing Xie ◽  
Qingbo Yu ◽  
Xin Yao ◽  
Wenjun Duan ◽  
Zongliang Zuo ◽  
...  

Author(s):  
Piyush Pratap Singh ◽  
Neelkanth Nirmalkar ◽  
Tarak Mondal

Catalytic steam reforming (SR) of agricultural waste derived bio-oil for hydrogen production is a unique technology, offering twin benefits of waste management as well as sustainable energy production. In the...


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